CN107008260A - A kind of preparation method of low paraffin dehydrogenation catalyst - Google Patents
A kind of preparation method of low paraffin dehydrogenation catalyst Download PDFInfo
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- CN107008260A CN107008260A CN201710403821.3A CN201710403821A CN107008260A CN 107008260 A CN107008260 A CN 107008260A CN 201710403821 A CN201710403821 A CN 201710403821A CN 107008260 A CN107008260 A CN 107008260A
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- Prior art keywords
- preparation
- dehydrogenation catalyst
- paraffin dehydrogenation
- alumina
- low paraffin
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- 239000003054 catalyst Substances 0.000 title claims abstract description 37
- 238000006356 dehydrogenation reaction Methods 0.000 title claims abstract description 31
- 238000002360 preparation method Methods 0.000 title claims abstract description 31
- 239000012188 paraffin wax Substances 0.000 title claims abstract description 27
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 51
- 239000012752 auxiliary agent Substances 0.000 claims abstract description 15
- 239000004480 active ingredient Substances 0.000 claims abstract description 8
- 230000037396 body weight Effects 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 11
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N EtOH Substances CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 10
- 229910052783 alkali metal Inorganic materials 0.000 claims description 9
- 150000001340 alkali metals Chemical class 0.000 claims description 9
- 238000007493 shaping process Methods 0.000 claims description 9
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 8
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 8
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 6
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 6
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 6
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims description 6
- 229910052700 potassium Inorganic materials 0.000 claims description 6
- 239000011591 potassium Substances 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 6
- 229910021627 Tin(IV) chloride Inorganic materials 0.000 claims description 5
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 229910052718 tin Inorganic materials 0.000 claims description 5
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 229910001593 boehmite Inorganic materials 0.000 claims description 4
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 239000011780 sodium chloride Substances 0.000 claims description 4
- 239000002202 Polyethylene glycol Substances 0.000 claims description 3
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 3
- 229910021502 aluminium hydroxide Inorganic materials 0.000 claims description 3
- 239000002585 base Substances 0.000 claims description 3
- 239000001913 cellulose Substances 0.000 claims description 3
- 229920002678 cellulose Polymers 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 230000001404 mediated effect Effects 0.000 claims description 3
- 150000007522 mineralic acids Chemical class 0.000 claims description 3
- 150000007524 organic acids Chemical class 0.000 claims description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 3
- 229920001223 polyethylene glycol Polymers 0.000 claims description 3
- 238000001125 extrusion Methods 0.000 claims description 2
- 238000005469 granulation Methods 0.000 claims description 2
- 230000003179 granulation Effects 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims 2
- 239000004411 aluminium Substances 0.000 claims 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 2
- 239000003292 glue Substances 0.000 claims 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims 1
- 244000275012 Sesbania cannabina Species 0.000 claims 1
- 239000000460 chlorine Substances 0.000 claims 1
- 229910052801 chlorine Inorganic materials 0.000 claims 1
- 230000000694 effects Effects 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 4
- 238000009826 distribution Methods 0.000 abstract description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 16
- 239000001294 propane Substances 0.000 description 8
- 238000005470 impregnation Methods 0.000 description 7
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 7
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 6
- 238000001035 drying Methods 0.000 description 6
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 6
- 206010013786 Dry skin Diseases 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 4
- 241000219782 Sesbania Species 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 239000001103 potassium chloride Substances 0.000 description 3
- 235000011164 potassium chloride Nutrition 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002808 molecular sieve Substances 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 2
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical compound CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 229910020944 Sn-Mg Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000013064 chemical raw material Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 238000005120 petroleum cracking Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/62—Platinum group metals with gallium, indium, thallium, germanium, tin or lead
- B01J23/622—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead
- B01J23/626—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead with tin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
- C07C5/333—Catalytic processes
- C07C5/3335—Catalytic processes with metals
- C07C5/3337—Catalytic processes with metals of the platinum group
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
The present invention provides a kind of preparation method of low paraffin dehydrogenation catalyst, comprises the following steps：S1, preparation θ alumina supports；S2, carrying active ingredients and auxiliary agent are in θ alumina supports.The present invention provides a kind of method for preparing low paraffin dehydrogenation catalyst by θ alumina supports, and to possess carbon distribution few, the characteristics of long lifespan.
Description
Technical field
The invention belongs to field of catalyst preparation, it is related to a kind of method of low paraffin dehydrogenation catalyst, particularly one kind
Method for preparing catalyst for the anti-carbon of preparing propylene by dehydrogenating propane.
Background technology
Propylene is a kind of important basic organic chemical raw material, and traditional production technology by petroleum cracking route is difficult to
Growing propylene demand is met, therefore, is existed in recent years using the technology of abundant and cheap Trends In Preparation of Propene By Catalytic Dehydrogenation of Propane
The country is developed rapidly.
The key of dehydrogenating propane technology is the exploitation of catalyst, has applied for Patents by Duo Jia research units both at home and abroad.
Traditional makees carrier for preparing propylene by dehydrogenating propane reaction, such as CN102049267A, CN102698750A with gama-alumina；Cause
This in recent years many patents propose with molecular sieve as carrier, such as CN106362791A, CN105148979A.
Aluminum oxide is catalyst common carrier, different with sintering temperature according to presoma species, can obtain different crystal forms.
Gama-alumina is big due to surface area, and aperture is small and abundant, beneficial to the scattered of active metal, is the crystal formation commonly used in catalyst.
Sintering temperature is conventional during the preparation of gama-alumina 300~700 DEG C, in higher temperature, are calcined, aperture at such as 800~1000 DEG C
Disappear, specific surface area is reduced, transformation of crystal is θ-aluminum oxide, and using common dipping method, active metal is difficult to disperse, therefore
The introducing of dispersion aids becomes extremely important.
Because dehydrogenating propane is strong endothermic reaction, reaction is carried out at high temperature, the easy coking of catalyst, in existing patent,
Either gama-alumina or molecular sieve, specific surface area it is big (>150m2/ g), containing more micropore, carbon distribution holds in production
Duct is easily blocked, causes the inactivation of catalyst fast, needs frequent regeneration.
The content of the invention
It is an object of the invention to provide a kind of preparation method of low paraffin dehydrogenation catalyst, solve in above-mentioned technical problem
One or more.
The present invention provides a kind of preparation method of low paraffin dehydrogenation catalyst, comprises the following steps：
S1, preparation θ-alumina support；
S2, carrying active ingredients and auxiliary agent are in θ-alumina support.
The present invention provides a kind of method that low paraffin dehydrogenation catalyst is prepared by θ-alumina support, and θ-aluminum oxide has
Following characteristics：Specific surface area 50-150m2/g；Aperture ＞ 20nm；Intensity ＞ 50N/；Therefore possess that carbon distribution is few, the spy of long lifespan
Point.
In some embodiments, the step of preparing θ-alumina support in S1, is mediated using Alumina gel and shaping assistant
Uniformly, extrude, granulate, drying, 900 DEG C~1050 DEG C roastings obtain θ-alumina support in 3~10 hours.
In some embodiments, the solute raw material of Alumina gel is at least one of boehmite, both boehmites,
The peptizing agent of Alumina gel is inorganic acid or organic acid.
In some embodiments, the solute raw material of Alumina gel also includes aluminium hydroxide.
In some embodiments, shaping assistant is sesbania powder, cellulose, polyethylene glycol, the weight of shaping assistant for θ-
The 4~8% of carrying alumina body weight.
In some embodiments, active component is Pt, active component weight for θ-carrying alumina body weight 0.1~
0.5%；
The step of carrying active ingredients is：θ-alumina support is immersed in the aqueous solution of potassium chloroplatinate, abundant saturation
Afterwards, take out, dry.
In some embodiments, S3,600 DEG C of roastings in addition to after S2.
In some embodiments, auxiliary agent includes Sn in S2, and Sn contents are the 0.1~2% of θ-carrying alumina body weight；
Load Sn auxiliary agents the step of be：θ-aluminum oxide is immersed in 50%SnCl4Ethanol solution in, after abundant saturation,
Take out, dry.
In some embodiments, auxiliary agent also includes alkali metal or alkaline-earth metal in S2, and alkali metal or alkaline-earth metal contain
Measure as the 0.1~1% of θ-carrying alumina body weight；
The step of carrying alkali metal or base earth metal promoter is：θ-aluminum oxide is immersed in magnesium chloride, sodium chloride, potassium chloride
Solution in, after abundant saturation, take out, dry.
Embodiment
The present invention provides a kind of preparation method of low paraffin dehydrogenation catalyst, comprises the following steps：
S1, preparation θ-alumina support；
S2, carrying active ingredients and auxiliary agent are in θ-alumina support.
The present invention provides a kind of method that low paraffin dehydrogenation catalyst is prepared by θ-alumina support, and θ-aluminum oxide has
Following characteristics：Specific surface area 50-150m2/g；Aperture ＞ 20nm；Intensity ＞ 50N/；Therefore possess that carbon distribution is few, the spy of long lifespan
Point.
In a kind of various embodiments of the preparation method for low paraffin dehydrogenation catalyst that the present invention is provided, prepared in S1
The step of θ-alumina support, it is preferable that
Mediated uniformly using Alumina gel and shaping additive, extrusion, granulation, dry, 900 DEG C~1050 DEG C roastings 3~10 are small
When obtain θ-alumina support.
In a kind of various embodiments of the preparation method for low paraffin dehydrogenation catalyst that the present invention is provided, prepared in S1
The step of θ-alumina support, it is preferable that
The solute raw material of Alumina gel is at least one of boehmite, both boehmites, and the peptizing agent of Alumina gel is
Inorganic acid or organic acid.
In a kind of various embodiments of the preparation method for low paraffin dehydrogenation catalyst that the present invention is provided, prepared in S1
The step of θ-alumina support, it is preferable that
The solute raw material of Alumina gel also includes aluminium hydroxide.
In a kind of various embodiments of the preparation method for low paraffin dehydrogenation catalyst that the present invention is provided, prepared in S1
The step of θ-alumina support, it is preferable that
Shaping assistant is sesbania powder, cellulose, polyethylene glycol, and the weight of shaping assistant is the 4 of θ-carrying alumina body weight
~8%.
It is excellent in S2 in a kind of various embodiments of the preparation method for low paraffin dehydrogenation catalyst that the present invention is provided
Choosing,
Active component is Pt, and active component weight is the 0.1~0.5% of θ-carrying alumina body weight；
The step of carrying active ingredients is：θ-alumina support is immersed in the aqueous solution of potassium chloroplatinate, abundant saturation
Afterwards, take out, dry.
In a kind of various embodiments of the preparation method for low paraffin dehydrogenation catalyst that the present invention is provided, it is preferable that also
Including the S3 after S2,600 DEG C of roastings.
In a kind of various embodiments of the preparation method for low paraffin dehydrogenation catalyst that the present invention is provided, it is preferable that S2
Middle auxiliary agent includes Sn, and Sn contents are the 0.1~2% of θ-carrying alumina body weight；
Load Sn auxiliary agents the step of be：θ-aluminum oxide is immersed in 50%SnCl4Ethanol solution in, after abundant saturation,
Take out, dry.
In a kind of various embodiments of the preparation method for low paraffin dehydrogenation catalyst that the present invention is provided, it is preferable that S2
Middle auxiliary agent also includes alkali metal or alkaline-earth metal, the content of alkali metal or alkaline-earth metal for θ-carrying alumina body weight 0.1~
1%；
The step of carrying alkali metal or base earth metal promoter is：θ-aluminum oxide is immersed in magnesium chloride, sodium chloride, potassium chloride
Solution in, after abundant saturation, take out, dry.
With reference to embodiment, the present invention is further detailed explanation.
Embodiment 1：
S1, preparation θ-alumina support；
By boehmite, 5% nitric acid of boehmite parts by weight, boehmite parts by weight 3%
Sesbania powder, is well mixed, and the kneading that adds water is agglomerating, and pelletizing is extruded with banded extruder, and disk is shaped to particle diameter 2mm ball；At 120 DEG C
Drying 12 hours, 1000 DEG C are calcined 3~10 hours, and carrier is made；The mass fraction of above-mentioned nitric acid is 65%.
S2, carrying active ingredients and auxiliary agent are in θ-alumina support；
Carrier impregnation is in 50%SnCl4Ethanol solution in, after abundant saturation, take out, under 80 DEG C of moving airs dry 8
Hour, Sn contents are 1.0% in carrier；
Again by carrier impregnation in the aqueous solution of potassium chloroplatinate and potassium chloride, after abundant saturation, take out, 120 DEG C of dryings 8 are small
When, Pt contents are 0.5% in sample, and potassium content is 0.8%.
S3,600 DEG C be calcined 4 hours, obtain supporting Pt-Sn-K propane dehydrogenation catalyst finished products.
Embodiment 2：
S1 carrier impregnation is in magnesium chloride solution in S2, Example 1, after abundant saturation, 105 DEG C of dryings 4 hours,
800 DEG C are calcined 4 hours, and magnesium 1.0% is contained in carrier；
Again by carrier impregnation in SnCl4In the mixed solution of chloroplatinic acid, after abundant saturation, take out, 120 DEG C of dryings 8 are small
When, Pt contents are that 0.3%, Sn contents are 0.3%；
S3, by carrier in 600 DEG C be calcined 4 hours, obtain Pt-Sn-Mg propane dehydrogenation catalyst finished products.
Embodiment 3：
S1 carrier impregnation is in SnCl in S2, Example 14Ethanol solution in, after abundant saturation, take out, at 80 DEG C
Dried 4 hours under moving air, Sn contents are 0.5% in carrier；
Carrier impregnation is in platinum acid chloride solution, after abundant saturation, takes out, and 250 DEG C are calcined 4 hours, and Pt contents are in sample
0.5%；
Again by carrier impregnation in sodium chloride solution, after abundant saturation, take out, 120 DEG C of dryings 4 hours, sodium contains in sample
Measure as 0.8%；
S3,600 DEG C of carrier are calcined 4 hours, obtain supporting Pt-Sn-Na propane dehydrogenation catalyst finished products.
Above-described is only some embodiments of the present invention.For the person of ordinary skill of the art, not
On the premise of departing from the invention design, various modifications and improvements can be made, these belong to the protection model of the present invention
Enclose.
Claims (9)
1. a kind of preparation method of low paraffin dehydrogenation catalyst, it is characterised in that comprise the following steps：
S1, preparation θ-alumina support；
S2, carrying active ingredients and auxiliary agent are in the θ-alumina support.
2. the preparation method of a kind of low paraffin dehydrogenation catalyst according to claim 1, it is characterised in that prepared in S1
The step of θ-alumina support, mediated using Alumina gel and shaping assistant it is uniform, extrusion, granulation, dry, 900 DEG C~1050 DEG C
Roasting obtains θ-alumina support in 3~10 hours.
3. the preparation method of a kind of low paraffin dehydrogenation catalyst according to claim 2, it is characterised in that the aluminium is molten
The solute raw material of glue is at least one of boehmite, both boehmites, the peptizing agent of the Alumina gel for inorganic acid or
Organic acid.
4. the preparation method of a kind of low paraffin dehydrogenation catalyst according to claim 3, it is characterised in that the aluminium is molten
The solute raw material of glue also includes aluminium hydroxide.
5. a kind of preparation method of low paraffin dehydrogenation catalyst according to claim 2, it is characterised in that the shaping
Auxiliary agent is sesbania powder, cellulose, polyethylene glycol, the weight of the shaping assistant for the θ-carrying alumina body weight 4~
8%.
6. a kind of preparation method of low paraffin dehydrogenation catalyst according to claim 1, it is characterised in that the activity
Composition is Pt, and active component weight is the 0.1~0.5% of the θ-carrying alumina body weight；
The step of carrying active ingredients is：θ-alumina support is immersed in the aqueous solution of potassium chloroplatinate, abundant saturation
Afterwards, take out, dry.
7. the preparation method of a kind of low paraffin dehydrogenation catalyst according to claim 1, it is characterised in that also including S2
S3 afterwards, 600 DEG C of roastings.
8. the preparation method of a kind of low paraffin dehydrogenation catalyst according to claim 1, it is characterised in that described in S2
Auxiliary agent includes Sn, and Sn contents are the 0.1~2% of the θ-carrying alumina body weight；
The step of loading the Sn auxiliary agents be：θ-the aluminum oxide is immersed in 50%SnCl4Ethanol solution in, abundant saturation
Afterwards, take out, dry.
9. the preparation method of a kind of low paraffin dehydrogenation catalyst according to claim 8, it is characterised in that described in S2
Auxiliary agent also includes alkali metal or alkaline-earth metal, and the content of the alkali metal or alkaline-earth metal is the θ-carrying alumina body weight
0.1~1%；
The step of loading the alkali metal or base earth metal promoter be：θ-the aluminum oxide is immersed in magnesium chloride, sodium chloride, chlorine
In the solution for changing potassium, after abundant saturation, take out, dry.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111632627A (en) * | 2020-05-18 | 2020-09-08 | 上海国惠环保科技集团有限公司 | Preparation method of structural auxiliary for molding |
| CN115487795A (en) * | 2021-06-18 | 2022-12-20 | 中国石油化工股份有限公司 | Spherical alumina carrier and preparation method thereof, dehydrogenation catalyst and application |
| CN115487856A (en) * | 2021-06-18 | 2022-12-20 | 中国石油化工股份有限公司 | Spherical esterification catalyst, preparation method thereof and application thereof in acetate synthesis reaction |
| CN115487852A (en) * | 2021-06-18 | 2022-12-20 | 中国石油化工股份有限公司 | Spherical non-noble metal catalyst, preparation method thereof and application thereof in preparation of propylene by propane dehydrogenation |
| CN115487851A (en) * | 2021-06-18 | 2022-12-20 | 中国石油化工股份有限公司 | Spherical dehydrogenation catalyst, preparation method thereof and application of spherical dehydrogenation catalyst in reaction for preparing isobutene through isobutane dehydrogenation |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101898130A (en) * | 2009-05-25 | 2010-12-01 | 中国石油化工股份有限公司 | Method for preparing dehydrogenation catalyst |
| CN102730724A (en) * | 2012-05-31 | 2012-10-17 | 江苏晶晶新材料有限公司 | Preparation process for large pore volume and light bulk density activated alumina |
| CN103480359A (en) * | 2013-09-26 | 2014-01-01 | 中国海洋石油总公司 | Preparation method for light alkane dehydrogenation catalyst with non-uniformly distributed active components |
| CN105312046A (en) * | 2015-11-05 | 2016-02-10 | 中国海洋石油总公司 | Light alkane dehydrogenation catalyst and method for improving activity and stability thereof |
-
2017
- 2017-06-01 CN CN201710403821.3A patent/CN107008260A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101898130A (en) * | 2009-05-25 | 2010-12-01 | 中国石油化工股份有限公司 | Method for preparing dehydrogenation catalyst |
| CN102730724A (en) * | 2012-05-31 | 2012-10-17 | 江苏晶晶新材料有限公司 | Preparation process for large pore volume and light bulk density activated alumina |
| CN103480359A (en) * | 2013-09-26 | 2014-01-01 | 中国海洋石油总公司 | Preparation method for light alkane dehydrogenation catalyst with non-uniformly distributed active components |
| CN105312046A (en) * | 2015-11-05 | 2016-02-10 | 中国海洋石油总公司 | Light alkane dehydrogenation catalyst and method for improving activity and stability thereof |
Non-Patent Citations (1)
| Title |
|---|
| U SHI ET AL.: ""Influence of support on the catalytic properties of Pt-Sn-K/θ-Al2O3 for propane dehydrogenation"", 《ROYAL SOCIETY OF CHEMISTRY》 * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111632627A (en) * | 2020-05-18 | 2020-09-08 | 上海国惠环保科技集团有限公司 | Preparation method of structural auxiliary for molding |
| CN115487795A (en) * | 2021-06-18 | 2022-12-20 | 中国石油化工股份有限公司 | Spherical alumina carrier and preparation method thereof, dehydrogenation catalyst and application |
| CN115487856A (en) * | 2021-06-18 | 2022-12-20 | 中国石油化工股份有限公司 | Spherical esterification catalyst, preparation method thereof and application thereof in acetate synthesis reaction |
| CN115487852A (en) * | 2021-06-18 | 2022-12-20 | 中国石油化工股份有限公司 | Spherical non-noble metal catalyst, preparation method thereof and application thereof in preparation of propylene by propane dehydrogenation |
| CN115487851A (en) * | 2021-06-18 | 2022-12-20 | 中国石油化工股份有限公司 | Spherical dehydrogenation catalyst, preparation method thereof and application of spherical dehydrogenation catalyst in reaction for preparing isobutene through isobutane dehydrogenation |
| CN115487852B (en) * | 2021-06-18 | 2024-06-04 | 中国石油化工股份有限公司 | Spherical non-noble metal catalyst, preparation method thereof and application thereof in propylene preparation by propane dehydrogenation |
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